EP3585846B1 - Calcium carbonate slurry - Google Patents
Calcium carbonate slurry Download PDFInfo
- Publication number
- EP3585846B1 EP3585846B1 EP18758348.9A EP18758348A EP3585846B1 EP 3585846 B1 EP3585846 B1 EP 3585846B1 EP 18758348 A EP18758348 A EP 18758348A EP 3585846 B1 EP3585846 B1 EP 3585846B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- calcium carbonate
- slurry
- particles
- dispersant
- substrate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 title claims description 320
- 239000002002 slurry Substances 0.000 title claims description 194
- 229910000019 calcium carbonate Inorganic materials 0.000 title claims description 160
- 239000002245 particle Substances 0.000 claims description 178
- 239000000758 substrate Substances 0.000 claims description 94
- 239000002270 dispersing agent Substances 0.000 claims description 66
- 239000007779 soft material Substances 0.000 claims description 44
- 238000005498 polishing Methods 0.000 claims description 37
- 238000000034 method Methods 0.000 claims description 27
- DBMJMQXJHONAFJ-UHFFFAOYSA-M Sodium laurylsulphate Chemical compound [Na+].CCCCCCCCCCCCOS([O-])(=O)=O DBMJMQXJHONAFJ-UHFFFAOYSA-M 0.000 claims description 22
- 238000006748 scratching Methods 0.000 claims description 22
- 230000002393 scratching effect Effects 0.000 claims description 22
- 229920001495 poly(sodium acrylate) polymer Polymers 0.000 claims description 20
- NNMHYFLPFNGQFZ-UHFFFAOYSA-M sodium polyacrylate Chemical compound [Na+].[O-]C(=O)C=C NNMHYFLPFNGQFZ-UHFFFAOYSA-M 0.000 claims description 20
- 239000000203 mixture Substances 0.000 claims description 18
- 239000003945 anionic surfactant Substances 0.000 claims description 17
- 238000003756 stirring Methods 0.000 claims description 16
- 239000000725 suspension Substances 0.000 claims description 16
- 238000002156 mixing Methods 0.000 claims description 15
- 239000000017 hydrogel Substances 0.000 claims description 13
- 239000000872 buffer Substances 0.000 claims description 10
- 229920000136 polysorbate Polymers 0.000 claims description 7
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 6
- 230000002572 peristaltic effect Effects 0.000 claims description 6
- 229910052708 sodium Inorganic materials 0.000 claims description 6
- 239000011734 sodium Substances 0.000 claims description 6
- SNXYIOIMZXSIDC-UHFFFAOYSA-A hexadecasodium;phosphonato phosphate Chemical compound [Na+].[Na+].[Na+].[Na+].[Na+].[Na+].[Na+].[Na+].[Na+].[Na+].[Na+].[Na+].[Na+].[Na+].[Na+].[Na+].[O-]P([O-])(=O)OP([O-])([O-])=O.[O-]P([O-])(=O)OP([O-])([O-])=O.[O-]P([O-])(=O)OP([O-])([O-])=O.[O-]P([O-])(=O)OP([O-])([O-])=O SNXYIOIMZXSIDC-UHFFFAOYSA-A 0.000 claims description 5
- 239000001509 sodium citrate Substances 0.000 claims description 5
- NLJMYIDDQXHKNR-UHFFFAOYSA-K sodium citrate Chemical compound O.O.[Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O NLJMYIDDQXHKNR-UHFFFAOYSA-K 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- JYCQQPHGFMYQCF-UHFFFAOYSA-N 4-tert-Octylphenol monoethoxylate Chemical compound CC(C)(C)CC(C)(C)C1=CC=C(OCCO)C=C1 JYCQQPHGFMYQCF-UHFFFAOYSA-N 0.000 claims description 4
- 239000002738 chelating agent Substances 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 229920002113 octoxynol Polymers 0.000 claims description 4
- 229950008882 polysorbate Drugs 0.000 claims description 4
- 229910021538 borax Inorganic materials 0.000 claims description 3
- UQGFMSUEHSUPRD-UHFFFAOYSA-N disodium;3,7-dioxido-2,4,6,8,9-pentaoxa-1,3,5,7-tetraborabicyclo[3.3.1]nonane Chemical compound [Na+].[Na+].O1B([O-])OB2OB([O-])OB1O2 UQGFMSUEHSUPRD-UHFFFAOYSA-N 0.000 claims description 3
- HWGNBUXHKFFFIH-UHFFFAOYSA-I pentasodium;[oxido(phosphonatooxy)phosphoryl] phosphate Chemical compound [Na+].[Na+].[Na+].[Na+].[Na+].[O-]P([O-])(=O)OP([O-])(=O)OP([O-])([O-])=O HWGNBUXHKFFFIH-UHFFFAOYSA-I 0.000 claims description 3
- 235000011083 sodium citrates Nutrition 0.000 claims description 3
- GCLGEJMYGQKIIW-UHFFFAOYSA-H sodium hexametaphosphate Chemical compound [Na]OP1(=O)OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])O1 GCLGEJMYGQKIIW-UHFFFAOYSA-H 0.000 claims description 3
- 235000019982 sodium hexametaphosphate Nutrition 0.000 claims description 3
- 235000010339 sodium tetraborate Nutrition 0.000 claims description 3
- 239000004328 sodium tetraborate Substances 0.000 claims description 3
- 235000019832 sodium triphosphate Nutrition 0.000 claims description 3
- 239000001577 tetrasodium phosphonato phosphate Substances 0.000 claims description 3
- 239000004094 surface-active agent Substances 0.000 description 41
- 239000000243 solution Substances 0.000 description 37
- 239000007787 solid Substances 0.000 description 19
- 239000011521 glass Substances 0.000 description 18
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 14
- 238000005259 measurement Methods 0.000 description 14
- LENZDBCJOHFCAS-UHFFFAOYSA-N tris Chemical compound OCC(N)(CO)CO LENZDBCJOHFCAS-UHFFFAOYSA-N 0.000 description 13
- 239000007788 liquid Substances 0.000 description 12
- 239000000463 material Substances 0.000 description 11
- 239000007983 Tris buffer Substances 0.000 description 10
- 238000004220 aggregation Methods 0.000 description 9
- 230000002776 aggregation Effects 0.000 description 9
- 239000000654 additive Substances 0.000 description 8
- 238000009826 distribution Methods 0.000 description 6
- 238000002296 dynamic light scattering Methods 0.000 description 6
- 239000000377 silicon dioxide Substances 0.000 description 6
- 238000013019 agitation Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 230000007246 mechanism Effects 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- CETPSERCERDGAM-UHFFFAOYSA-N ceric oxide Chemical compound O=[Ce]=O CETPSERCERDGAM-UHFFFAOYSA-N 0.000 description 4
- 229910000422 cerium(IV) oxide Inorganic materials 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- 229920000058 polyacrylate Polymers 0.000 description 4
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 3
- 238000009472 formulation Methods 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 230000005653 Brownian motion process Effects 0.000 description 2
- QPCDCPDFJACHGM-UHFFFAOYSA-N N,N-bis{2-[bis(carboxymethyl)amino]ethyl}glycine Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(=O)O)CCN(CC(O)=O)CC(O)=O QPCDCPDFJACHGM-UHFFFAOYSA-N 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 238000005537 brownian motion Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 239000000314 lubricant Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 108020004707 nucleic acids Proteins 0.000 description 2
- 150000007523 nucleic acids Chemical group 0.000 description 2
- 102000039446 nucleic acids Human genes 0.000 description 2
- 229960003330 pentetic acid Drugs 0.000 description 2
- 239000002861 polymer material Substances 0.000 description 2
- 239000004065 semiconductor Substances 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L sodium carbonate Substances [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 229920002125 Sokalan® Polymers 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 230000004931 aggregating effect Effects 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 150000007942 carboxylates Chemical group 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000001246 colloidal dispersion Methods 0.000 description 1
- 230000002596 correlated effect Effects 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 238000009499 grossing Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000000693 micelle Substances 0.000 description 1
- 238000001127 nanoimprint lithography Methods 0.000 description 1
- MGFYIUFZLHCRTH-UHFFFAOYSA-N nitrilotriacetic acid Chemical compound OC(=O)CN(CC(O)=O)CC(O)=O MGFYIUFZLHCRTH-UHFFFAOYSA-N 0.000 description 1
- 238000000399 optical microscopy Methods 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 238000007517 polishing process Methods 0.000 description 1
- 229920002401 polyacrylamide Polymers 0.000 description 1
- 239000004584 polyacrylic acid Substances 0.000 description 1
- 229920002959 polymer blend Polymers 0.000 description 1
- 229920006254 polymer film Polymers 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 239000001488 sodium phosphate Substances 0.000 description 1
- 229910000162 sodium phosphate Inorganic materials 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
- 230000007480 spreading Effects 0.000 description 1
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 description 1
- RYFMWSXOAZQYPI-UHFFFAOYSA-K trisodium phosphate Chemical compound [Na+].[Na+].[Na+].[O-]P([O-])([O-])=O RYFMWSXOAZQYPI-UHFFFAOYSA-K 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09G—POLISHING COMPOSITIONS; SKI WAXES
- C09G1/00—Polishing compositions
- C09G1/02—Polishing compositions containing abrasives or grinding agents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B24—GRINDING; POLISHING
- B24C—ABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
- B24C1/00—Methods for use of abrasive blasting for producing particular effects; Use of auxiliary equipment in connection with such methods
- B24C1/08—Methods for use of abrasive blasting for producing particular effects; Use of auxiliary equipment in connection with such methods for polishing surfaces, e.g. smoothing a surface by making use of liquid-borne abrasives
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B24—GRINDING; POLISHING
- B24B—MACHINES, DEVICES, OR PROCESSES FOR GRINDING OR POLISHING; DRESSING OR CONDITIONING OF ABRADING SURFACES; FEEDING OF GRINDING, POLISHING, OR LAPPING AGENTS
- B24B1/00—Processes of grinding or polishing; Use of auxiliary equipment in connection with such processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B24—GRINDING; POLISHING
- B24B—MACHINES, DEVICES, OR PROCESSES FOR GRINDING OR POLISHING; DRESSING OR CONDITIONING OF ABRADING SURFACES; FEEDING OF GRINDING, POLISHING, OR LAPPING AGENTS
- B24B37/00—Lapping machines or devices; Accessories
- B24B37/04—Lapping machines or devices; Accessories designed for working plane surfaces
- B24B37/042—Lapping machines or devices; Accessories designed for working plane surfaces operating processes therefor
- B24B37/044—Lapping machines or devices; Accessories designed for working plane surfaces operating processes therefor characterised by the composition of the lapping agent
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09G—POLISHING COMPOSITIONS; SKI WAXES
- C09G1/00—Polishing compositions
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09G—POLISHING COMPOSITIONS; SKI WAXES
- C09G1/00—Polishing compositions
- C09G1/04—Aqueous dispersions
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09G—POLISHING COMPOSITIONS; SKI WAXES
- C09G1/00—Polishing compositions
- C09G1/06—Other polishing compositions
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K13/00—Etching, surface-brightening or pickling compositions
- C09K13/04—Etching, surface-brightening or pickling compositions containing an inorganic acid
- C09K13/06—Etching, surface-brightening or pickling compositions containing an inorganic acid with organic material
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K3/00—Materials not provided for elsewhere
- C09K3/14—Anti-slip materials; Abrasives
- C09K3/1409—Abrasive particles per se
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K3/00—Materials not provided for elsewhere
- C09K3/14—Anti-slip materials; Abrasives
- C09K3/1454—Abrasive powders, suspensions and pastes for polishing
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K3/00—Materials not provided for elsewhere
- C09K3/14—Anti-slip materials; Abrasives
- C09K3/1454—Abrasive powders, suspensions and pastes for polishing
- C09K3/1463—Aqueous liquid suspensions
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/02—Manufacture or treatment of semiconductor devices or of parts thereof
- H01L21/04—Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer
- H01L21/18—Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer the devices having semiconductor bodies comprising elements of Group IV of the Periodic Table or AIIIBV compounds with or without impurities, e.g. doping materials
- H01L21/30—Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26
- H01L21/302—Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26 to change their surface-physical characteristics or shape, e.g. etching, polishing, cutting
- H01L21/306—Chemical or electrical treatment, e.g. electrolytic etching
- H01L21/30625—With simultaneous mechanical treatment, e.g. mechanico-chemical polishing
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/02—Manufacture or treatment of semiconductor devices or of parts thereof
- H01L21/04—Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer
- H01L21/18—Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer the devices having semiconductor bodies comprising elements of Group IV of the Periodic Table or AIIIBV compounds with or without impurities, e.g. doping materials
- H01L21/30—Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26
- H01L21/31—Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26 to form insulating layers thereon, e.g. for masking or by using photolithographic techniques; After treatment of these layers; Selection of materials for these layers
- H01L21/3205—Deposition of non-insulating-, e.g. conductive- or resistive-, layers on insulating layers; After-treatment of these layers
- H01L21/321—After treatment
- H01L21/32115—Planarisation
- H01L21/3212—Planarisation by chemical mechanical polishing [CMP]
Definitions
- CMP chemical mechanical polishing
- substrates including silica and ceria polishing slurries.
- CMP chemical mechanical polishing
- These commercialized slurries may be useful in polishing oxide films and metals on a substrate, but they may be undesirable in polishing soft materials, including polymer films such as polymeric hydrogels, that may be easily susceptible to scratching.
- Substrates may be coated with soft materials and may include nanoscale features. For example, a glass substrate coated with a soft material may be used in gene sequencer systems as well as in other biological or chemical analysis systems.
- WO97/11585A1 A method of modifying an exposed surface of a semiconductor wafer.
- a composition is provided as defined in claim 1. In some implementations, less than about 5% of a total number of the calcium carbonate particles has a diameter greater than about 4 ⁇ m.
- a method for polishing a surface of a substrate with a calcium carbonate slurry, where the substrate is coated with a soft material, where the calcium carbonate slurry is as defined herein.
- the soft material includes an organic polymeric hydrogel.
- the method further includes mixing, prior to polishing the substrate, the plurality of calcium carbonate particles in the solution with the dispersant and the anionic surfactant using one or more of a magnetic stir bar, impeller type mixer, diaphragm pump, slurry pump, peristaltic pump, and high pressure pump.
- the substrate includes a plurality of features, each of the features having a diameter between about 1 nm and about 100 nm. In some implementations, polishing the surface of the substrate coated with the soft material occurs without substantially scratching the surface of the substrate.
- a method for manufacturing a calcium carbonate slurry as defined herein comprising mixing a dispersant and an anionic surfactant into a solution and adding a plurality of calcium carbonate particles suspended in the solution to form a slurry, where a concentration of the calcium carbonate particles in the slurry is equal to or less than about 2.0 wt.%.
- the method further includes mixing the plurality of calcium carbonate particles over time to maintain suspension of the calcium carbonate particles in the solution.
- the present disclosure provides a slurry, and more particularly a slurry with calcium carbonate particles that remain in suspension over a relatively long period of time and are relatively resistant to aggregation.
- the slurry with calcium carbonate particles remains in suspension for at least six days (e.g., seven, eight, nine, ten, twenty, or more) and is relatively resistant to aggregating by having a zeta potential that is equal to or less than -50 mV.
- the slurry may be used in polishing substrates, including substrates coated with soft materials.
- soft materials can include any polymer material or monomeric material that is cured or crosslinked.
- a slurry with large particles or aggregates of particles may cause scratching during the polishing of soft materials from a substrate.
- An effective slurry formulation of the present disclosure may include relatively small calcium carbonate particles, a relatively low concentration of calcium carbonate particles, a dispersant, and a surfactant, where the dispersant and the surfactant may keep the particles in suspension over time and reduce aggregation.
- a slurry of the present disclosure includes at least a dispersant and a surfactant.
- the slurry further includes a plurality of calcium carbonate particles suspended in a solution, where the solution includes the dispersant and the surfactant.
- the solution may further include a buffer.
- An average diameter of the plurality of calcium carbonate particles is between about 10 nm and about 3 ⁇ m, between about 30 nm and about 2 ⁇ m, between about 300 nm and about 2 ⁇ m, or between about 500 nm and about 1 ⁇ m, where the term "about” with respect to the average diameter of the calcium carbonate particles refers to values within plus or minus 5 percent of the stated value
- the concentration of the calcium carbonate in the slurry is equal to or less than about 2.0 wt.%, between about 0.05 wt.% and about 1.0 wt.%, between about 0.1 wt.% and about 1.0 wt.%, or between about 0.1 wt.% and about 0.5 wt.%., where the term "about” with respect to the concentration of calcium carbonate throughout this disclosure refers to values within plus or minus 5 percent of the stated value.
- the dispersant may serve to stabilize particle distributions in the solution.
- the dispersant may be selected to reduce a zeta potential of the slurry, where a more negative zeta potential indicates that particles are more likely to repel each other and less likely to form aggregates.
- the zeta potential of the slurry is equal to or less than about -50 mV.
- the dispersants include sodium polyacrylate, sodium n-silicate, sodium tetrapyrophosphate, sodium hexametaphosphate, sodium polyalluminate, sodium tetraborate, sodium triphosphate, and sodium citrate.
- One or both of the dispersant and the surfactant may serve to stabilize the turbidity of the slurry.
- the surfactant may serve as a lubricant that lowers the surface tension between two liquids or between a liquid and a solid.
- the slurry may include an anionic surfactant that limits surface charge buildup, thereby reducing the zeta potential so that particles will not aggregate together.
- the surfactants include sodium dodecyl sulfate (SDS), polysorbate, and octylphenol ethoxylate.
- SDS sodium dodecyl sulfate
- polysorbate polysorbate
- octylphenol ethoxylate octylphenol ethoxylate.
- the pH of the slurry can be between about 7 and about 12, such as between about 8.5 and about 10.5.
- a substrate can refer to a solid support.
- the term includes any material that can serve as a solid or semi-solid foundation for features such as wells or channels for the deposition of nucleic acids.
- a substrate can include any appropriate substrate materials, including but not limited to glass, modified glass, functionalized glass, silica, quartz, silicon, plastic, metal, metal oxide, or combinations thereof.
- modified glass includes a thick layer (e.g., greater than about 5 nm) of material on glass that changes one or more properties of the glass, functional glass includes a covalent or semi-covalent bond on the surface of glass, and silica includes a type of glass with a different base composition than traditional glass, where the term "about" with respect to the thickness of the thick layer of the modified glass throughout this disclosure refers to values within plus or minus 10 percent of the stated value.
- the substrate includes a cured polymer mixture on glass, such as a nanoimprinted resist material on glass.
- the substrate can include one or more features.
- a feature can refer to a discrete physical element or discrete physical trait of a substrate.
- a discrete physical element can include a component of the substrate that is physically or structurally distinguishable.
- a discrete physical trait of a substrate can include an aspect of the substrate itself that provides physical or functional separability.
- features of the substrate can be in the form of a well or channel, which may be discrete physical elements of the substrate.
- the substrate may be part of an array for biological or chemical analysis systems. Sequencers, such as DNA or RNA sequencers and other biological or chemical analysis systems, may utilize a glass substrate having microfluidic flow channels provided therein.
- a nano-feature can have a diameter between 0.5 nm and about 500 nm, between about 1 nm and about 100 nm, or between about 5 nm and about 50 nm, where the term "about" with respect to a diameter of a feature throughout this disclosure refers to values within plus or minus 10 percent of the stated value.
- Soft materials may be part of a substrate or coated on a substrate, where a soft material can include any polymer material or monomeric material that is cured or crosslinked.
- a substrate may be coated with a soft material, including but not limited to a polymer, an inorganic hydrogel, or an organic polymeric hydrogel.
- the soft material can include a polyacrylamide hydrogel. Sequencers may rely on attachment of nucleic acid strands to a hydrogel-coated surface of a substrate during operation.
- a substrate may be made out of a soft material, including but not limited to a silicon-hydrocarbon array.
- the substrate may be coated with more than one layer of soft material.
- a substrate surface may be coated with a resist layer, and an organic polymeric hydrogel may be formed on the resist layer.
- the resist layer and the organic polymeric hydrogel may be deemed "soft.”
- the resist layer is a nanoimprinted polymeric resist material coated via nanoimprint lithography methods.
- polishing a substrate can refer to mechanical and/or chemical treatment of a substrate.
- polishing can refer to removal of a part of a substrate or a coating on a substrate.
- Polishing can refer to rubbing, chafing, smoothing, or otherwise treating a surface of a substrate to produce an altered surface of the substrate.
- Polishing a substrate coated with soft materials may involve removal of at least some of the soft materials from the substrate.
- the substrate may be coated with a first soft material and a second soft material, where the second soft material has a hardness less than the first soft material, and polishing the substrate may involve removal of the second soft material without removal of the first soft material.
- a substrate surface may include a resist layer coated with an acrylate polymer layer that is softer than the resist layer, where polishing the substrate can include removal of the acrylate polymer layer without damaging the resist layer.
- the surface of the substrate may be susceptible to scratching.
- an underlying layer upon which the soft material is formed upon may be susceptible to scratching.
- the surface of the substrate that is susceptible to scratching may include such layers. For example, where a surface of a substrate includes a resist layer and a softer acrylate polymer layer is disposed over the resist layer, the acrylate polymer layer is polished but the resist layer may be scratched by pre-existing slurries.
- soft materials coated on or part of a substrate are difficult to optimize with pre-existing slurries and have quicker feature gouging, which involves particles digging into surface features during polishing to cause excess removal of material in one area.
- a pre-existing slurry such as a silica and ceria polishing slurry, may scratch the surface of the substrate and leave particles in nano-features of the substrate.
- pre-existing methods using formulations without particles exhibit high variability during polishing, require a long run time, have difficulty cleaning nano-features, and require a high pressure that can lead to substrate breakage and strain on the polisher.
- the present disclosure provides in some examples a composition including a slurry, where the slurry includes a plurality of particles in a liquid.
- the composition of the present disclosure consists of or consists essentially of the slurry.
- a "slurry" can refer to a fluid mixture including particles in a liquid.
- a calcium carbonate slurry includes particles of calcium carbonate in a liquid.
- a calcium carbonate slurry is capable of polishing or removing soft materials coated on a substrate or part of the substrate.
- calcium carbonate particles in the slurry are generally softer than ceria or silica particles, and are less likely to scratch a surface of a substrate during polishing.
- calcium carbonate slurries are generally cheaper than ceria or silica slurries.
- large calcium carbonate particles or small calcium carbonate particles that aggregate to a large size will scratch the surface of the substrate during polishing, thereby decreasing the performance and quality of the slurry.
- An effective calcium carbonate slurry may be formulated that keeps the calcium carbonate particles in suspension for a long period of time and is resistant to aggregation of the calcium carbonate particles. This allows the calcium carbonate slurry to polish soft materials from the surface of the substrate with less scratching of the surface in a more robust and reproducible manner compared to pre-existing slurries.
- the performance or quality of the polish may be correlated with the formulation of the calcium carbonate slurry in terms of size of the particles in the slurry, the particles' tendency towards aggregation, and the consistency of the solids delivery.
- the size of the particles in the slurry may be measured by dynamic light scattering (DLS), the particles' tendency towards aggregation may correspond to a zeta potential of the slurry, and the consistency of solids delivery may be determined at least in part using turbidity.
- DLS dynamic light scattering
- Particle size may be determined using DLS.
- DLS uses a laser to scatter light off of particles undergoing Brownian motion, determining the particles' speed. Knowing the viscosity and temperature of the particle, a DLS instrument calculates the size of the particle. Larger particles undergo slower Brownian motion and smaller particles move faster. DLS can determine the size distribution of particles and the percentage of particles having a diameter equal to or greater than a threshold diameter, such as having a diameter equal to or greater than about 4 ⁇ m.
- a polish can be adversely affected by the presence of large particles in the slurry.
- Some of the large particles may include aggregates of smaller particles.
- the term "large particles” or “oversized particles” include particles having a diameter equal to or greater than a threshold diameter, or aggregates of smaller particles having a diameter equal to or greater than the threshold diameter.
- a threshold diameter may be about 3 ⁇ m, about 4 ⁇ m, about 5 ⁇ m, about 6 ⁇ m, about 7 ⁇ m, about 8 ⁇ m, about 9 ⁇ m, or about 10 ⁇ m.
- a threshold diameter for a large particle or an oversized particle may depend on various factors such as the composition of the substrate, the composition of the slurry, pressure applied during polishing, size of surface features, potential for surface damage, polishing pad choice, material that a glass is functionalized with (e.g., if this material is softer, it may be more susceptible to scratching), etc.
- a threshold diameter for a large particle or an oversized particle may be equal to or greater than about 4 ⁇ m when polishing soft materials on a glass substrate, where particles having a diameter equal to or greater than 4 ⁇ m may be capable of scratching the surface of the glass substrate. Scratching on a polished surface may be determined using an imager and a microscope.
- the size distribution of the plurality of particles has less than about 10%, less than about 5%, or less than about 3% of a total number of particles equal to or greater than the threshold diameter.
- the calcium carbonate slurry may include a plurality of particles suspended in a solution, where an average diameter of the plurality of calcium carbonate particles is between about 10 nm and about 3 ⁇ m, between about 30 nm and about 2 ⁇ m, between about 300 nm and about 2 ⁇ m, or between about 500 nm and about 1 ⁇ m, where the term "about" with respect to an average diameter of the plurality of calcium carbonate particles throughout this disclosure refers to values within plus or minus 5 percent of the stated value.
- a standard deviation for an average diameter of the calcium carbonate particles can be within plus or minus 120 nm.
- the calcium carbonate slurry may include a plurality of particles suspended in a solution, where less than about 5% of a total number of the calcium carbonate particles have a diameter equal to or greater than about 4 ⁇ m, where the term "about” with respect to a percentage of the total number of calcium carbonate particles throughout this disclosure refers to values within plus or minus 5 percent of the stated value.
- Zeta potential is an indicator of the stability of colloidal dispersions and serves as a metric to determine the propensity of particles in a slurry to aggregate.
- Zeta potential can refer to an electric potential in an electrical double layer at the location of a slipping plane for a particle relative to a point in the liquid away from the electrical double layer.
- the electrical double layer is a layer that appears on a surface of a particle when exposed to a fluid, which can include charged species that move in the fluid under the influence of electric attraction and thermal motion.
- zeta potential can be measured using a Malvern Zetasizer. A more negative zeta potential is indicative that particles in the slurry will strongly repel each other and are less likely to form aggregates. A more positive zeta potential is indicative that particles in the slurry will attract each other and are more likely to form aggregates.
- the ionic strength of the solution may have an effect on zeta potential.
- the ionic strength of the solution may be adjusted by a buffer and a concentration of the buffer.
- the concentration of the buffer may be adjusted by diluting it in a solvent, such as water.
- the buffer can include tris(hydroxymethyl)aminomethane (TRIS) buffer.
- TriS tris(hydroxymethyl)aminomethane
- Other possible buffers include but are not limited to sodium phosphate, sodium citrate, and sodium carbonate.
- the buffer may be able to achieve a pH between 9 and 12 in the solution.
- a TRIS buffer may be diluted to a desired concentration.
- a 0.1 M TRIS buffer may be diluted by deionized water to get a concentration between about 0.01 M and about 0.05 M, or between about 0.02 M and about 0.04 M.
- the solution can further include a chelating agent, such as ethylenediaminetetraacetic acid (EDTA).
- EDTA ethylenediaminetetraacetic acid
- Other chelating agents include but are not limited to diethylenetriaminepentaacetic acid (DTPA) and nitrilotriacetic acid (NTA).
- DTPA diethylenetriaminepentaacetic acid
- NTA nitrilotriacetic acid
- the chelating agent may be capable of sequestering metal ions, such as calcium ions, in solution.
- Additives may be introduced to the slurry to reduce (i.e., make more negative) the zeta potential of the slurry.
- Additives for reducing the zeta potential of the slurry can include but are not limited to a dispersant and a surfactant. Such additives can be considered part of a solution of a calcium carbonate slurry, whereas calcium carbonate particles as discussed herein can be considered suspended in the solution of the calcium carbonate slurry.
- a calcium carbonate slurry with one or more additives has a zeta potential of about -50 mV or less, or of about -60 mV or less, where the term "about” with respect to zeta potential of the slurry throughout this disclosure refers to values within plus or minus 5 percent of the stated value.
- a dispersant is an agent that is used to stabilize particle distributions in liquid systems. It can include a polymer or molecule added to a suspension to improve separation of particles in the suspension. The dispersant increases the electrical double layer of the particles in the suspension to reduce aggregation.
- the dispersants added to a calcium carbonate slurry can be sodium polyacrylate of various molecular weights, sodium n-silicate, sodium tetrapyrophosphate, sodium hexametaphosphate, sodium polyalluminate, sodium tetraborate, sodium triphosphate, sodium citrate, or combinations thereof.
- the dispersant has a concentration in the slurry between about 0.1 wt.% and about 0.5 wt.%.
- Figure 1 shows example data illustrating zeta potential of calcium carbonate slurries with various dispersants.
- the calcium carbonate slurry in Figure 1 included 0.125 wt.% 2 ⁇ m calcium carbonate particles with 0.03 M TRIS buffer at pH 10.4.
- Four different dispersants were tested: sodium polyacrylate with molecular weight 15,000, sodium polyacrylate with molecular weight 1,200, sodium tetrapyrophosphate, and sodium citrate. Each of these dispersants was added to the solution at a concentration of 0.25 wt.% in the slurry. Data from a control slurry (no dispersant) is also shown.
- the molecular weight of the dispersant can influence the tendency of particles to aggregate in the slurry. In some examples, if the molecular weight is too small, short chains in the dispersant will not provide a sufficiently thick barrier to prevent flocculation, which leads to adhesion of particles suspended in solution to form larger-size clusters. If the molecular weight is too large, however, the dispersant will start to act as a flocculant.
- Figure 2 shows example data illustrating zeta potential for calcium carbonate slurries with various molecular weights of sodium polyacrylate dispersant.
- Sodium polyacrylate comes in different molecular weights, and selection of an appropriate molecular weight may be important in lowering zeta potential.
- the calcium carbonate slurry in Figure 2 included 0.125 wt.% 2 ⁇ m calcium carbonate particles with 0.03 M TRIS buffer at pH 10.4.
- Sodium polyacrylate at four different molecular weights of 15,000, 8,000, 5,100, and 1,200 were added at 0.25 wt.% to each sample of calcium carbonate slurry and tested.
- the concentration of the dispersant in the slurry also can influence the tendency of particles to aggregate. If the concentration of the dispersant is too low, dispersant molecules adsorbed to the particles may only partially cover each of the particles and provide limited performance in increasing the electrical double layer of the particle. If the concentration of the dispersant is too high, the molecular structure of dispersant molecules adsorbed to the particles may collapse or "fold back" on themselves, thereby allowing particles to aggregate or flocculate.
- Figures 3A and 3B show example data illustrating zeta potential for calcium carbonate slurries with different concentrations of sodium polyacrylate dispersant in one non-limiting working example.
- Figure 3A shows zeta potential data for sodium polyacrylate dispersant concentrations between 0.025 wt.% and 25.0 wt.%.
- Figure 3B shows zeta potential data for sodium polyacrylate dispersant concentrations between 0.1 wt.% and 0.5 wt.%.
- the sodium polyacrylate had a molecular weight of 1,200.
- the calcium carbonate slurry in Figures 3A and 3B included 0.125 wt.% 2 ⁇ m calcium carbonate particles with 0.03 M TRIS buffer at pH 10.4.
- a surfactant is an agent that assists in the spreading of one phase into another, whether in solid-liquid systems or liquid-liquid systems.
- the surfactant serves to lower the surface tension between two liquids or between a liquid and a solid. In other words, the surfactant can act like a lubricant.
- the surfactant added to the slurry is an anionic surfactant.
- An anionic surfactant contains an anionic functional group at one end, such as a sulfate, sulfonate, phosphate, and carboxylate functional group.
- the anionic surfactant may prevent surface charge buildup from being too high on calcium carbonate particles. That way, the calcium carbonate particles do not aggregate.
- the surfactants added to a calcium carbonate slurry can be sodium dodecyl sulfate (SDS), polysorbate, octylphenol ethoxylate, or combinations thereof.
- SDS sodium dodecyl sulfate
- Tween® 20 is an example of a polysorbate and TritonTM X-100 is an example of an octylphenol ethoxylate.
- Tween® 20 is manufactured by Croda International plc of East Riding of England, UK TritonTM X-100 is manufactured by Rohm and Haas Company of Philadelphia, PA, USA.
- the concentration of the surfactant may depend on the critical micellar concentration of the surfactant.
- the critical micellar concentration is the surfactant concentration above which the surfactant will form micelles in the solution.
- the surfactant has a concentration in the slurry of between about 0.01 wt.% and about 10.0 wt.%, between about 0.05 wt.% and about 5.0 wt.%, or between about 0.1 wt.% and about 2.0 wt.%, where the term "about” with respect to surfactant concentration in the slurry throughout this disclosure refers to values within plus or minus 10 percent of the stated value.
- Figure 4 shows example data illustrating zeta potential of calcium carbonate slurries with various surfactants.
- the calcium carbonate slurry in Figure 4 included 0.125 wt.% 2 ⁇ m calcium carbonate particles with 0.03 M TRIS buffer at pH 10.4.
- Three different surfactants were tested: SDS, Tween® 20, and TritonTM X-100. Each of these surfactants were added at a concentration of 0.125 wt.%.
- addition of a surfactant in the calcium carbonate slurry reduces the zeta potential of the slurry.
- SDS as a surfactant had the greatest effect on zeta potential among the tested surfactants in Figure 4 .
- a surfactant and a dispersant may be added to a solution of a slurry.
- the combination of the surfactant and the dispersant in the slurry can have an even greater effect on zeta potential than a surfactant individually or a dispersant individually.
- Figure 5 shows example data illustrating zeta potential of calcium carbonate slurries with various dispersants combined with SDS surfactant.
- the calcium carbonate slurry in Figure 5 included 0.125 wt.% 2 ⁇ m calcium carbonate particles with 0.03 M TRIS buffer at pH 10.4.
- Sodium polyacrylate combined with SDS had a zeta potential that was more negative than sodium tetrapyrophosphate combined with SDS. Accordingly, sodium polyacrylate combined with SDS was more effective in reducing zeta potential of the slurry.
- the pH of the slurry may affect the zeta potential of the slurry.
- a pH that is closer to the pKa of calcium carbonate is likely to have a lower zeta potential.
- the pKa of calcium carbonate is about 9.
- the pH of the slurry may affect the performance and quality of the slurry, where both positive and negative extremes of pH can be harmful.
- calcium carbonate particles dissolve.
- the calcium carbonate slurry can corrode electrodes and damage flow cell chemistry of a substrate.
- the pH of the calcium carbonate slurry is between about 7 and about 12, such as between about 8.5 and about 10.5, where the term "about" with respect to pH throughout this disclosure refers to values within plus or minus 5 percent of the stated value. In a particular example, the pH of the calcium carbonate slurry may be about 9.
- Figure 6 shows example data illustrating zeta potential of calcium carbonate slurries at different pH.
- the calcium carbonate slurries in Figure 6 included 0.125 wt.% 2 ⁇ m calcium carbonate particles with 0.125 wt.% SDS and with 0.03 M TRIS buffer.
- Figure 6 shows that the pH of the slurry affects the zeta potential of the slurry.
- the calcium carbonate slurry had a more negative zeta potential at pH 10.4 than at pH 7.5. This may be due in part to the dissolution of calcium carbonate particles at lower pH values.
- Turbidity is a measurement of the cloudiness or haziness of a fluid caused by particles suspended in the liquid. If turbidity is too low, the calcium carbonate particles may settle rather than remain in suspension after a period of time. This may adversely limit the effectiveness of polishing a substrate with a calcium carbonate slurry.
- a unit of measurement of turbidity is Nephelometric Turbidity Unit (NTU), which is a measurement of the amount of light scattered at a 90 degree angle from an incident light beam by particles. The settling rate of the particles and how well the particles to remain in suspension can be determined by taking turbidity measurements over a period of time. A reduced turbidity measurement over time is indicative of particles settling faster and not remaining in suspension.
- NTU Nephelometric Turbidity Unit
- Figure 7 shows example data illustrating turbidity of a calcium carbonate slurry without additives and a calcium carbonate slurry with a dispersant and surfactant. Turbidity was measured every 15 minutes over the course of an hour for a control slurry having 0.0625 wt.% 2 ⁇ m calcium carbonate particles with 0.05 M TRIS buffer at pH 9. The control slurry did not have a surfactant or a dispersant. Turbidity also was measured every 15 minutes over the course of an hour for the same slurry but added with 0.25 wt.% sodium polyacrylate having molecular weight of 1,200 and added with 0.125 wt.% SDS.
- the control slurry reduced in turbidity, indicating that the absence of a dispersant and a surfactant increases the settling rate of the particles in the slurry.
- the calcium carbonate slurry with a dispersant and with a surfactant maintained a substantially similar turbidity, indicating that the presence of a dispersant and/or a surfactant stabilizes the slurry.
- Addition of a dispersant and/or surfactant may contribute to keeping calcium carbonate particles in suspension over a long period of time.
- FIGS 8A-8D show images of calcium carbonate slurries with different sizes of calcium carbonate particles after 2 hours, 4 hours, 7 hours, and 24 hours.
- Each calcium carbonate slurry sample included 0.125 wt.% calcium carbonate, 0.125 wt.% SDS, 0.25 wt.% polyacrylic acid, 1 mM EDTA, and 0.1 M TRIS at pH 9.
- One sample included 2 ⁇ m calcium carbonate particles, two samples included 0.7 ⁇ m calcium carbonate particles, and one sample included 0.2 ⁇ m particles. After 24 hours, the settling rate of the 2 ⁇ m calcium carbonate particles was noticeably greater than the others. Smaller particles may have a slower settling rate than larger particles.
- mixing or agitation mechanisms can be utilized to circulate or mix the plurality of calcium carbonate particles in the solution.
- Such a mixing or agitation mechanism can keep the percent solids constant, increase the shelf life of the slurry with constant mixing, and prevent or otherwise reduce the formation of aggregates that are undesirable to polishing quality.
- the mixing or agitation mechanism also may fracture some of the particles to a smaller size. Examples of mixing or agitation mechanisms include but are not limited to a diaphragm pump, a magnetic stir bar, an impeller-type mixer, a slurry pump, a peristaltic pump, and a high pressure pump.
- Particles or aggregates having a diameter equal to or greater than a certain threshold diameter may be deemed oversized and harmful.
- particles or aggregates having a diameter greater than about 4 ⁇ m may be deemed oversized and harmful.
- other threshold diameters for establishing harmful or oversized particles or aggregates are appropriate. Utilization of a mixing or agitation mechanism prior to polishing may limit aggregation of particles into oversized particles.
- Figure 9A shows example data illustrating a percentage of oversized calcium carbonate particles over time for a 2 ⁇ m slurry mixed with a diaphragm pump and a 2 ⁇ m slurry mixed with a stir bar.
- an X ⁇ m slurry refers to a slurry with particles having an average diameter of X ⁇ m
- a Y nm slurry refers to a slurry with particles having an average diameter of Y nm.
- the standard deviation for the average diameter may be plus or minus 120 nm or plus or minus 400 nm.
- oversized particles are particles that are over 4 ⁇ m in diameter. After three days, roughly 4% of a total number of calcium carbonate particles were above 4 ⁇ m in diameter for both pumps. After six days, almost 10% of the total number of calcium carbonate particles were above 4 ⁇ m in diameter for both pumps.
- Figure 9B shows example data illustrating a percentage of oversized calcium carbonate particles over time for a 700 nm slurry mixed with a diaphragm pump and a 700 nm slurry mixed with a stir bar. Even after 6 days, less than 2% of the total number of calcium carbonate particles were above 4 ⁇ m in diameter for both pumps.
- Figures 9A and 9B show that it may take fewer 2 ⁇ m particles than 700 nm particles to aggregate to a harmful size.
- the settling rate of particles can be measured using percent solids measurements in addition to or instead of turbidity measurements.
- Percent solids measurements can be made by comparing a sample weight before and after being centrifuged, aspirated, and dried. For example, percent solids measurements were made for slurries having 0.25 wt.% calcium carbonate particles with 0.25 wt.% sodium polyacrylate, 0.125 wt.% SDS, and TRIS buffer at pH 9. The percent solids measurements were made across a span of seven days, where a 1 mL aliquot was taken each day and dried in a 60°C oven for an hour, and a weight difference was measured.
- Figure 10A shows example data illustrating percent solids measurements for a 2 ⁇ m slurry mixed with a stir bar and a 2 ⁇ m slurry mixed with a diaphragm pump.
- Figure 10B shows example data illustrating percent solids measurements for a 700 nm slurry mixed with a stir bar and a 700 nm slurry mixed with a diaphragm pump.
- the amount of solids in the diaphragm pump decreased sharply while the stir bar percent solids remained roughly the same.
- the stir bar was more effective in keeping particles suspended.
- the quality of a polished surface can be determined in part by the amount of scratching on the polished surface using an imager and a microscope.
- scratching on a polished surface of a substrate can be determined using a Nikon high resolution imager and a Zeiss confocal microscope.
- the calcium carbonate slurry may polish one or more soft materials coated on a substrate without scratching or substantially scratching an underlying layer.
- substantially in the context of scratching refers to the presence of any scratches having a size that is equal to or larger than 1 ⁇ m when observed using optical microscopy.
- Figures 11A-11C show a series of images of substrates polished using a calcium carbonate slurry.
- Figure 11A shows an image of a substrate polished with 2 ⁇ m particles and with dispersant. Some scratching of the substrate appeared near the edges of the substrate.
- Figure 11B shows an image of a substrate polished with 2.5 ⁇ m calcium carbonate slurry
- Figure 11C shows an image of a substrate polished with a 4.5 ⁇ m calcium carbonate slurry. The substrate polished using large particles exhibited more scratching than the substrate polished using smaller particles.
- Figure 12 shows a flow diagram illustrating an example method for polishing a surface of a substrate.
- the method 1200 may be performed with different, fewer, or additional operations.
- a surface of a substrate is polished with a calcium carbonate slurry, where the substrate is coated with a soft material.
- the calcium carbonate slurry includes a dispersant, an anionic surfactant, and a plurality of calcium carbonate particles suspended in a solution.
- the plurality of calcium carbonate particles are optionally mixed in the solution including the dispersant and the anionic surfactant to form the calcium carbonate slurry.
- the mixing may occur using one or more of a magnetic stir bar, impeller type mixer, diaphragm pump, slurry pump, peristaltic pump, and high pressure pump.
- a concentration of the calcium carbonate particles in the calcium carbonate slurry is equal to or less than about 2.0 wt.%.
- the soft material can include a polymer, an inorganic hydrogel, or an organic polymeric hydrogel.
- the soft material can include an organic polymeric hydrogel.
- the substrate includes a plurality of features, each of the features has a diameter between about 0.5 nm and about 500 nm, between about 1 nm and about 100 nm, or between about 5 nm and about 50 nm.
- polishing the surface of the substrate coated with the soft material occurs without substantially scratching the surface of the substrate.
- One or both of the dispersant and the anionic surfactant reduces a zeta potential of the slurry.
- the zeta potential of the slurry is equal to or less than about -50 mV.
- Figure 13 shows a flow diagram illustrating an example method for manufacturing a calcium carbonate slurry.
- the method 1300 may be performed with different, fewer, or additional operations.
- a dispersant and an anionic surfactant are mixed into a solution.
- the solution may have a desired ionic strength.
- the solution includes one or both of a buffer and water.
- a plurality of calcium carbonate particles are added in the solution to form a slurry, where a concentration of the calcium carbonate particles in the slurry is equal to or less than about 2.0 wt.%. In some implementations, the concentration of the calcium carbonate particles in the slurry is between about 0.05 wt.% and about 1.0 wt.%.
- the plurality of calcium carbonate particles may be suspended in the solution.
- the zeta potential of the slurry is equal to or less than about -50 mV, or equal to or less than about -60 mV.
- An average diameter of the plurality of calcium carbonate particles is between about 10 nm and about 3 ⁇ m, between about 30 nm and about 2 ⁇ m, between about 300 nm and about 2 ⁇ m, or between about 500 nm and about 1 ⁇ m. In some implementations, less than about 5% of a total number of the calcium carbonate particles has a diameter greater than about 4 ⁇ m.
- the plurality of calcium carbonate particles are optionally mixed over time to maintain suspension of the calcium carbonate particles in the solution.
- the plurality of calcium carbonate particles may be suspended in the solution for at least six days.
- the plurality of calcium carbonate particles may be mixed using one or more of a magnetic stir bar, impeller type mixer, diaphragm pump, slurry pump, peristaltic pump, and high pressure pump.
- a composition can be formulated that includes a stable calcium carbonate slurry, where the slurry includes a plurality of calcium carbonate particles suspended in a solution, the solution including a dispersant and a surfactant.
- concentration of the plurality of calcium carbonate particles in the slurry equal to or less than about 2.0 wt.%, or between about 0.05 wt.% and about 1.0 wt.%.
- An average diameter of the plurality of calcium carbonate particles is between about 10 nm and about 3 ⁇ m, between about 30 nm and about 2 ⁇ m, between about 300 nm and about 2 ⁇ m, or between about 500 nm and about 1 ⁇ m.
- less than about 5% of a total number of the calcium carbonate particles has a diameter greater than about 4 ⁇ m.
- the dispersant and the surfactant can be configured to reduce a zeta potential of the slurry to equal to or less than about -50 mV, or equal to or less than about -60 mV.
- the concentration of the dispersant in the slurry is between about 0.1 wt.% and about 0.5 wt.%.
- the calcium carbonate slurry may be resistant to aggregation and may remain in suspension for a long period of time.
- the composition of the calcium carbonate slurry as described above can be implemented in a method of polishing a substrate.
- the substrate comprises at least partly a soft material or is coated with a soft material.
- the soft material may include an organic polymeric hydrogel.
- the substrate can include a plurality of features, where each of the features has a diameter between about 0.5 nm and about 500 nm, between about 1 nm and about 100 nm, or between about 5 nm and about 50 nm. Polishing the substrate with the soft material or coated with the soft material can occur without substantially scratching the substrate.
- the method further includes mixing, prior to polishing the substrate, the plurality of calcium carbonate particles in the solution with the dispersant and the anionic surfactant using one or more of a magnetic stir bar, impeller type mixer, diaphragm pump, slurry pump, peristaltic pump, and high pressure pump.
- a magnetic stir bar impeller type mixer
- diaphragm pump diaphragm pump
- slurry pump peristaltic pump
- high pressure pump high pressure pump
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Microelectronics & Electronic Packaging (AREA)
- Condensed Matter Physics & Semiconductors (AREA)
- General Physics & Mathematics (AREA)
- Manufacturing & Machinery (AREA)
- Computer Hardware Design (AREA)
- Physics & Mathematics (AREA)
- Power Engineering (AREA)
- Inorganic Chemistry (AREA)
- Dispersion Chemistry (AREA)
- Finish Polishing, Edge Sharpening, And Grinding By Specific Grinding Devices (AREA)
- Mechanical Treatment Of Semiconductor (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
- Coloring Foods And Improving Nutritive Qualities (AREA)
- Disintegrating Or Milling (AREA)
- Crystals, And After-Treatments Of Crystals (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Detergent Compositions (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201762463533P | 2017-02-24 | 2017-02-24 | |
PCT/US2018/019019 WO2018156629A1 (en) | 2017-02-24 | 2018-02-21 | Calcium carbonate slurry |
Publications (3)
Publication Number | Publication Date |
---|---|
EP3585846A1 EP3585846A1 (en) | 2020-01-01 |
EP3585846A4 EP3585846A4 (en) | 2020-10-14 |
EP3585846B1 true EP3585846B1 (en) | 2021-11-10 |
Family
ID=63254311
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP18758348.9A Active EP3585846B1 (en) | 2017-02-24 | 2018-02-21 | Calcium carbonate slurry |
Country Status (13)
Country | Link |
---|---|
US (2) | US11214712B2 (zh) |
EP (1) | EP3585846B1 (zh) |
JP (1) | JP6955569B2 (zh) |
KR (1) | KR102370056B1 (zh) |
CN (1) | CN110546221B (zh) |
AU (1) | AU2018225631B2 (zh) |
CA (1) | CA3053175C (zh) |
ES (1) | ES2904456T3 (zh) |
IL (1) | IL268613B2 (zh) |
SA (1) | SA519402469B1 (zh) |
SG (1) | SG11201907230RA (zh) |
TW (1) | TWI665274B (zh) |
WO (1) | WO2018156629A1 (zh) |
Family Cites Families (35)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3245819A (en) | 1962-07-30 | 1966-04-12 | Wyandotte Chemicals Corp | Stabilization of calcium carbonate slurries |
US4040988A (en) * | 1974-09-27 | 1977-08-09 | The Procter & Gamble Company | Builder system and detergent product |
US4758377A (en) | 1985-09-24 | 1988-07-19 | The Proctor & Gamble Company | Viscous phase stable liquid scouring cleansers containing solvent |
JPH01187930A (ja) * | 1988-01-22 | 1989-07-27 | Nippon Telegr & Teleph Corp <Ntt> | 研磨剤及び研磨方法 |
JP2926408B2 (ja) * | 1989-04-19 | 1999-07-28 | ソマール株式会社 | 炭酸カルシウム水分散液及びその製造方法 |
US5279755A (en) * | 1991-09-16 | 1994-01-18 | The Clorox Company | Thickening aqueous abrasive cleaner with improved colloidal stability |
US5631523A (en) | 1995-09-19 | 1997-05-20 | Beacon Light Products, Inc. | Method of regulating lamp current through a fluorescent lamp by pulse energizing a driving supply |
US5958794A (en) * | 1995-09-22 | 1999-09-28 | Minnesota Mining And Manufacturing Company | Method of modifying an exposed surface of a semiconductor wafer |
GB9611701D0 (en) | 1996-06-05 | 1996-08-07 | Ecc Int Ltd | Particulate materials |
US5958288A (en) | 1996-11-26 | 1999-09-28 | Cabot Corporation | Composition and slurry useful for metal CMP |
ZA9710639B (en) | 1996-12-13 | 1998-06-15 | Minerals Tech Inc | Dewatering of calcium carbonate. |
US6294105B1 (en) | 1997-12-23 | 2001-09-25 | International Business Machines Corporation | Chemical mechanical polishing slurry and method for polishing metal/oxide layers |
KR100851451B1 (ko) | 1998-12-25 | 2008-08-08 | 히다치 가세고교 가부시끼가이샤 | Cmp 연마제, cmp 연마제용 첨가액 및 기판의 연마방법 |
EP1022326A1 (en) * | 1999-01-20 | 2000-07-26 | The Procter & Gamble Company | Hard surface cleaning compositions comprising modified alkylbenzene sulfonates |
JP4296362B2 (ja) | 1999-05-17 | 2009-07-15 | 上村工業株式会社 | 研磨剤組成物 |
KR20030037676A (ko) * | 2001-11-07 | 2003-05-14 | 삼성전자주식회사 | 반도체 웨이퍼 폴리싱용 슬러리 |
US7445769B2 (en) * | 2002-10-31 | 2008-11-04 | Cadbury Adams Usa Llc | Compositions for removing stains from dental surfaces and methods of making and using the same |
US6803353B2 (en) * | 2002-11-12 | 2004-10-12 | Atofina Chemicals, Inc. | Copper chemical mechanical polishing solutions using sulfonated amphiprotic agents |
EP1735394A4 (en) * | 2004-02-10 | 2011-07-20 | Vanderbilt Co R T | POLISH |
CN100545092C (zh) * | 2005-06-24 | 2009-09-30 | 上海华明高技术(集团)有限公司 | 一种亚微米级超细碳酸钙分散颗粒的制备方法 |
US8628737B2 (en) | 2006-11-09 | 2014-01-14 | Nalco Company | Transfer of slurry in a bayer process |
WO2009040597A1 (en) * | 2007-09-28 | 2009-04-02 | Laboratorio Chimico Farmaceutico Sammarinese S.A. | Liquid cleaning composition and method of cleaning a surface |
CN101570343B (zh) | 2009-06-11 | 2011-07-13 | 福建省万旗非金属材料有限公司 | 一种湿法制备水溶性油墨专用纳米碳酸钙的方法 |
AU2012355705B2 (en) * | 2011-12-22 | 2016-02-11 | Rohm And Haas Company | Calcium carbonate slurries |
US9512422B2 (en) * | 2013-02-26 | 2016-12-06 | Illumina, Inc. | Gel patterned surfaces |
AU2014284584B2 (en) | 2013-07-01 | 2019-08-01 | Illumina, Inc. | Catalyst-free surface functionalization and polymer grafting |
ES2763863T3 (es) * | 2014-04-28 | 2020-06-01 | Visionaturolab Inc | Composición para el cuidado bucal que comprende polvo de jibión y utilizaciones de la misma |
CN104131297B (zh) | 2014-07-01 | 2015-10-28 | 安徽宏发节能设备有限公司 | 一种纯铝以及铝合金铸件的化学抛光液及其制备方法 |
CN104087246A (zh) * | 2014-07-11 | 2014-10-08 | 司徒建辉 | 一种陶瓷研磨剂 |
JP6559410B2 (ja) | 2014-09-30 | 2019-08-14 | 株式会社フジミインコーポレーテッド | 研磨用組成物 |
US10179870B2 (en) * | 2014-12-05 | 2019-01-15 | 3M Innovative Properties Company | Abrasive composition |
EP3045503A1 (en) | 2015-01-15 | 2016-07-20 | Omya International AG | Surface-treated calcium carbonate with improved stability in environments with a pH of 4.5 to 7 |
US9803109B2 (en) | 2015-02-03 | 2017-10-31 | Cabot Microelectronics Corporation | CMP composition for silicon nitride removal |
CN106046860B (zh) | 2016-06-15 | 2018-12-21 | 江西广源化工有限责任公司 | 白炭黑/纳米钙复合浆料包覆湿法超细碳酸钙的制备方法 |
CN106318220A (zh) * | 2016-08-18 | 2017-01-11 | 江苏锦阳不锈钢制品有限公司 | 一种不锈钢表面加工用抛光液 |
-
2018
- 2018-02-21 KR KR1020197024390A patent/KR102370056B1/ko active IP Right Grant
- 2018-02-21 JP JP2019544915A patent/JP6955569B2/ja active Active
- 2018-02-21 IL IL268613A patent/IL268613B2/en unknown
- 2018-02-21 SG SG11201907230RA patent/SG11201907230RA/en unknown
- 2018-02-21 CN CN201880013157.4A patent/CN110546221B/zh active Active
- 2018-02-21 EP EP18758348.9A patent/EP3585846B1/en active Active
- 2018-02-21 ES ES18758348T patent/ES2904456T3/es active Active
- 2018-02-21 US US16/488,140 patent/US11214712B2/en active Active
- 2018-02-21 AU AU2018225631A patent/AU2018225631B2/en active Active
- 2018-02-21 WO PCT/US2018/019019 patent/WO2018156629A1/en unknown
- 2018-02-21 CA CA3053175A patent/CA3053175C/en active Active
- 2018-02-23 TW TW107106161A patent/TWI665274B/zh active
-
2019
- 2019-08-18 SA SA519402469A patent/SA519402469B1/ar unknown
-
2021
- 2021-12-06 US US17/543,642 patent/US11806836B2/en active Active
Also Published As
Publication number | Publication date |
---|---|
US20220089910A1 (en) | 2022-03-24 |
JP2020508575A (ja) | 2020-03-19 |
US11214712B2 (en) | 2022-01-04 |
ES2904456T3 (es) | 2022-04-05 |
BR112019016384A2 (pt) | 2020-04-07 |
EP3585846A1 (en) | 2020-01-01 |
US20200002575A1 (en) | 2020-01-02 |
SA519402469B1 (ar) | 2023-01-09 |
KR20190112739A (ko) | 2019-10-07 |
KR102370056B1 (ko) | 2022-03-03 |
NZ755991A (en) | 2021-10-29 |
EP3585846A4 (en) | 2020-10-14 |
AU2018225631B2 (en) | 2020-11-05 |
US11806836B2 (en) | 2023-11-07 |
IL268613B1 (en) | 2023-06-01 |
SG11201907230RA (en) | 2019-09-27 |
IL268613B2 (en) | 2023-10-01 |
WO2018156629A1 (en) | 2018-08-30 |
IL268613A (en) | 2019-09-26 |
CA3053175C (en) | 2023-02-28 |
AU2018225631A1 (en) | 2019-08-22 |
CA3053175A1 (en) | 2018-08-30 |
TW201831625A (zh) | 2018-09-01 |
JP6955569B2 (ja) | 2021-10-27 |
CN110546221A (zh) | 2019-12-06 |
TWI665274B (zh) | 2019-07-11 |
CN110546221B (zh) | 2022-02-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Dylla-Spears et al. | Charged micelle halo mechanism for agglomeration reduction in metal oxide particle based polishing slurries | |
TWI624536B (zh) | Polishing composition, polishing composition manufacturing method, and polishing product manufacturing method | |
Lemelle et al. | Curvature reversal of the circular motion of swimming bacteria probes for slip at solid/liquid interfaces | |
US20070094936A1 (en) | Abrasive slurry having high dispersion stability and manufacturing method for a substrate | |
US20190249122A1 (en) | Rinsing agent composition for silicon wafers | |
KR101970858B1 (ko) | 연마용 조성물 및 반도체 기판의 제조 방법 | |
WO2013157554A1 (ja) | シリコンウェーハ用研磨液組成物 | |
EP2106426B1 (de) | Zusammensetzung zum polieren von oberflächen aus siliziumdioxid | |
WO2015098197A1 (ja) | 研磨剤、研磨剤セット及び基体の研磨方法 | |
CN101351260B (zh) | 用于微通道分离的基质和动态聚合物体系和组合物 | |
CN1858131A (zh) | 用于铌酸锂光学晶片研磨抛光的抛光液 | |
US11806836B2 (en) | Calcium carbonate slurry | |
NZ755991B2 (en) | Calcium carbonate slurry | |
WO2008058196A2 (en) | Chemical mechanical polishing of moisture sensitive surfaces and compositions therefor | |
Zhong et al. | Effects of humic acid on recoverability and fractal structure of alum-kaolin flocs | |
BR112019016384B1 (pt) | Pasta fluida de carbonato de cálcio | |
JP6403324B2 (ja) | シリコンウェーハ用研磨液組成物 | |
JP2001277106A (ja) | 研磨方法及び研磨装置 | |
Wang et al. | Effect of temperature on the stability of aqueous ZrO2 suspensions | |
JP6367113B2 (ja) | シリコンウェーハ用研磨液組成物 | |
CN118280831A (zh) | 抛光液和基底表面处理方法 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE INTERNATIONAL PUBLICATION HAS BEEN MADE |
|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE |
|
17P | Request for examination filed |
Effective date: 20190923 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
AX | Request for extension of the european patent |
Extension state: BA ME |
|
RIN1 | Information on inventor provided before grant (corrected) |
Inventor name: BRITTELLE, SAMANTHA K. Inventor name: BAILEY, SCOTT WILLIAM Inventor name: YANG, ROBERT Inventor name: CHENG, YOU-JUNG Inventor name: TSAY, JAMES M. |
|
DAV | Request for validation of the european patent (deleted) | ||
DAX | Request for extension of the european patent (deleted) | ||
A4 | Supplementary search report drawn up and despatched |
Effective date: 20200916 |
|
RIC1 | Information provided on ipc code assigned before grant |
Ipc: C09K 3/14 20060101ALI20200910BHEP Ipc: C09G 1/02 20060101AFI20200910BHEP |
|
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: GRANT OF PATENT IS INTENDED |
|
INTG | Intention to grant announced |
Effective date: 20210614 |
|
GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE PATENT HAS BEEN GRANTED |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: REF Ref document number: 1446079 Country of ref document: AT Kind code of ref document: T Effective date: 20211115 Ref country code: CH Ref legal event code: EP |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R096 Ref document number: 602018026508 Country of ref document: DE |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: LT Ref legal event code: MG9D |
|
REG | Reference to a national code |
Ref country code: NL Ref legal event code: MP Effective date: 20211110 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2904456 Country of ref document: ES Kind code of ref document: T3 Effective date: 20220405 |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: MK05 Ref document number: 1446079 Country of ref document: AT Kind code of ref document: T Effective date: 20211110 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: RS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 Ref country code: LT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 Ref country code: FI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 Ref country code: BG Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20220210 Ref country code: AT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20220310 Ref country code: SE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 Ref country code: PT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20220310 Ref country code: PL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 Ref country code: NO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20220210 Ref country code: NL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 Ref country code: LV Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 Ref country code: HR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20220211 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SM Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 Ref country code: SK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 Ref country code: RO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 Ref country code: EE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 Ref country code: DK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 Ref country code: CZ Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R097 Ref document number: 602018026508 Country of ref document: DE |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MC Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
26N | No opposition filed |
Effective date: 20220811 |
|
REG | Reference to a national code |
Ref country code: BE Ref legal event code: MM Effective date: 20220228 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20220221 Ref country code: AL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20220228 Ref country code: IE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20220221 Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20220228 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20220228 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 |
|
P01 | Opt-out of the competence of the unified patent court (upc) registered |
Effective date: 20230511 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: ES Payment date: 20240319 Year of fee payment: 7 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 Ref country code: CY Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20240216 Year of fee payment: 7 Ref country code: GB Payment date: 20240222 Year of fee payment: 7 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: HU Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO Effective date: 20180221 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 20240222 Year of fee payment: 7 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: TR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211110 |